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JPH0442357B2 - - Google Patents
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JPH0442357B2 - - Google Patents

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Publication number
JPH0442357B2
JPH0442357B2 JP59000298A JP29884A JPH0442357B2 JP H0442357 B2 JPH0442357 B2 JP H0442357B2 JP 59000298 A JP59000298 A JP 59000298A JP 29884 A JP29884 A JP 29884A JP H0442357 B2 JPH0442357 B2 JP H0442357B2
Authority
JP
Japan
Prior art keywords
fertilizer
powdered
weight
mixture
parts
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59000298A
Other languages
Japanese (ja)
Other versions
JPS60145984A (en
Inventor
Hideki Tomohiro
Tsukasa Matsuda
Hidekazu Ikeda
Kazuo Izumida
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Chemical Industrial Co Ltd
Original Assignee
Nippon Chemical Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Chemical Industrial Co Ltd filed Critical Nippon Chemical Industrial Co Ltd
Priority to JP29884A priority Critical patent/JPS60145984A/en
Publication of JPS60145984A publication Critical patent/JPS60145984A/en
Publication of JPH0442357B2 publication Critical patent/JPH0442357B2/ja
Granted legal-status Critical Current

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  • Fertilizers (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は混合肥料造粒物の製法、更に言えば、
粉末溶成燐肥と粉末珪酸質肥料との混合肥料造粒
物に関する。 近年農業の近代化に伴ない施肥の省力化を目的
として数種類の肥料を混じてバルクブレンデイン
グしたものを機械散布する方法が行なわれている
が、これは粒状肥料を対象としたものであつて溶
成燐肥および珪酸質肥料混合物のような所謂細粒
肥料には分級が激しく適用できない。 そこで従来より、溶成燐肥および珪酸質肥料混
合物の造粒法がいくつか試みられておりバインダ
ーとして種々のものが提案がされている。例えば
バルブ廃液使用による造粒・該廃液とベントナイ
トの混用による造粒・尿素を用いるもの、ニトロ
フミン酸を用いるもの、アルコール醗酵廃液固型
分を用いるもの、ベントナイトを用いるものなど
がある。 又、運搬、貯蔵などに耐えるだけの充分な強
度、適度な見掛比重、発塵のない、しかも手ざわ
り良好な造粒物が要求され、かかる目的で粉末状
溶成燐肥および珪酸質肥料混合物の造粒について
はアルコール醗酵廃液などの主として有機性の副
生物をバインダーとして造粒品を得ることが開発
されている。しかしながら、このような副産物を
用いて造粒する場合、その主産物の生産量に支配
され易いので供給上の安定がなされないのみなら
ず、品質にもバラツキが生じ易い。また加えて、
アルコール醗酵廃液等の副生物は臭気が強く、か
つ腐敗してBOD含有量が高いため、作業環境を
悪化するのみならず、BODの除去費用も必要と
なるなどの欠点がある。 本発明者らは上述の問題に鑑み、より工業的に
有利な造粒品を得るべく研究したところ、驚くべ
きことに、硫酸マグネシウムがすぐれたバインダ
ーであることを知見し、本発明を完成した。 すなわち、本発明は、粉末溶成燐肥及び粉末珪
酸質肥料の混合物と結合剤よりなる混合肥料造粒
物の製法において、該粉末混合物を比表面積500
〜3000cm2/g、粒度44μm以下のもの10〜60重量
%とし、その粉末混合物100重量部と結合剤とし
て硫酸マグネシウム含有物1〜7重量部
(MgSO4換算)との配合物に適量の水を加えて造
粒し、70〜120℃で乾燥することを特徴とする混
合肥料造粒物の製法に関するものである。 本発明において適用される粉末溶成燐肥は、一
般に用いられているものとなんら変りなく、これ
は燐鉱石と蛇絞岩、かんらん岩またはニツケル精
錬などの珪酸マグネシウム系鉱物とを所定割合に
混合したものを加熱溶融した後水等で急冷し粉砕
したりして得られるガラス状粉末である。 なおこの場合硼素、マンガン、銅、亜鉛、また
はモリブデン等の微量要素成分を必要に応じて該
溶成燐肥に存在させたものであつてもよい。 又、本発明において適用される粉末珪酸質肥料
は、一般にケイカル、苦土ケイカルと呼ばれるも
ので、可溶性珪酸、アルカリ分、く溶性マグネシ
ウム等を含有するものであり、例えば、製銑鉱
滓、普通鋼鉱滓、ステンレス鋼鉱滓、フエロマン
ガン鋼鉱滓、シリコマンガン鉱滓、フエロニツケ
ル鉱滓、ニツケル鉱滓、フエロクロム鉱滓、マグ
ネシウム鉱滓、製リン残滓等を原料とするもので
ある。 粉末溶成燐肥と粉末珪酸質肥料との混合物の粒
度や比表面積は用いるバインダーの性質と共に造
粒化した場合の物性に著しく影響を与えるので所
定の範囲のものに調整しておくことが必要である
が、本発明において上記二つの粉末肥料混合物は
比表面積として500〜3000cm2/g、粒径としては
44μ以下が10〜60%含んでいるものが最も好適で
あり、この範囲を外れると水崩壊性と造粒強度と
が相矛盾する特性の要求を満足することは難かし
くなる傾向となる。 次に、本発明において上記二つの粉末肥料混合
物を造粒するに当つて、硫酸マグネシウム含有物
をバインダーとして用いるものであるが、これは
工業用硫酸マグネシウムは勿論、水酸化マグネシ
ウムと硫酸との反応生成物、マグネシアと硫酸と
の反応生成物、蛇絞岩またはかんらん岩と硫酸と
の反応生成物等も含まれ、MgSO4を主材とする
ものであるがほかに多少のMgCl2、Mg(OH)2
含んでも差支えない。 従つて、その性質上多少の未反応マグネシウム
等が混入していても、実質的に硫酸マグネシウム
を含有していれば差支えなく使用することがで
き、また、上記含有物は結晶品または水溶液のい
ずれのものであつてもよい。 粉末溶成燐肥および粉末珪酸質肥料の混合肥料
に対する硫酸マグネシウム含有物の使用量は、製
造条件や該混合物の物性によつて一様ではない
が、多くの場合、該粉末混合物100重量部当り、
MgSO4として1〜7重量部、好ましくは2〜4
重量部の範囲が適当である。 その理由は、1重量部未満では造粒が困難とな
り、他方7重量部より大となると経済的でないば
かりでなく、肥効成分との兼ねあいで不都合が生
じるからである。 上記二つの粉末肥料混合物に硫酸マグネシウム
含有物を用いて造粒するには従来の造粒法を特に
限定なく例えば皿型造粒機、ドラム造粒機または
圧縮成型機(圧べん造粒機)などの所望の造粒機
を用いて、適当量の水を添加しながら造粒し、次
いで温度70〜120℃で実質的な脱水物に至るまで
乾燥し要すれば分級して製品とする。 なお、上記乾燥条件でなければ、下記所定の粒
度の造粒物が歩留りよく得られないのみならず、
造粒物の貯蔵や運搬に耐える強度の造粒物となら
ないからである。 造粒物の大きさは用途によつて一様でないが、
多くの場合0.5〜5mm好ましくは1〜4mmの範囲
が適当であり、この範囲外のものは最初の工程に
戻して再利用する。 かくして、本発明の製法によれば、従来、粒状
にすることが困難であつた粉末溶成燐肥および粉
末珪酸質肥料の混合物を、その粒度調整と硫酸マ
グネシウム含有物を用いることによつて所望の大
きさに造粒することができる。 また、得られた混合肥料造粒物は、可溶性苦土
および硫酸根が付与されており、他の肥料とブレ
ンドして機械散布することができ、しかも水崩壊
性および土中崩壊性も良好なものである。 更に、適度な強度、見掛比重、発塵のない手ざ
わりも良好であると共に有機物をバインダーとし
て使用した造粒品に比べて悪臭防止法、水汚染防
止法、土壤汚染防止法、労働衛生法等の諸法規に
対して何ら問題を生じることなく製造でき、また
使用に当つて安全にとりあつかうことができるの
で、本発明の工業的意義は大きい。 以下、本発明について、実施例をあげて、具体
的に説明する。 実施例 1〜10 表−1に示す粉状溶成燐肥および粉末珪酸質肥
料の混合物に硫酸マグネシウム含有物の所定量を
添加した混合物を皿型造粒機(径1000m/m、深
さ80m/m、回転数12r.p.m、傾斜角54゜)に入れ
水をスプレーし、粒径が1〜4mm(望ましくは2
〜3mm)となるまで造粒する。これを乾燥し(70
〜120℃)水分0.1%以下とする。このものを冷却
後1〜4m/mになるまで整粒し、この割合を歩
留率とし、粉末溶成燐肥および粉末珪酸質肥料の
混合肥料造粒物を得た。このものについて平均圧
壊強度、水崩壊性、土中崩壊性の試験結果を表1
に示す。
The present invention provides a method for producing mixed fertilizer granules, and more specifically,
This invention relates to a mixed fertilizer granule of powdered dissolved phosphorous fertilizer and powdered silicic acid fertilizer. In recent years, with the modernization of agriculture, a method of mechanically distributing a bulk blend of several types of fertilizers has been used to save labor in fertilization, but this method is only intended for granular fertilizers. Classification is severely inapplicable to so-called fine-grained fertilizers such as dissolved phosphorous fertilizers and siliceous fertilizer mixtures. Therefore, several methods of granulating dissolved phosphorous fertilizers and siliceous fertilizer mixtures have been attempted, and various binders have been proposed. Examples include granulation by using valve waste liquid, granulation by mixing the waste liquid with bentonite, urea, nitrofumic acid, alcohol fermentation waste liquid solids, and bentonite. In addition, granules are required that have sufficient strength to withstand transportation, storage, etc., appropriate apparent specific gravity, do not generate dust, and have a good texture. Regarding granulation, it has been developed to obtain granulated products using mainly organic by-products such as alcohol fermentation waste liquid as a binder. However, when granulation is performed using such by-products, the production volume of the main product tends to be controlled, so not only is the supply not stable, but the quality is also likely to vary. In addition,
By-products such as alcohol fermentation waste liquid have a strong odor, putrefaction, and high BOD content, which not only deteriorates the working environment but also requires the cost of BOD removal. In view of the above problems, the present inventors conducted research to obtain a granulated product that is more industrially advantageous, and surprisingly discovered that magnesium sulfate is an excellent binder, and completed the present invention. . That is, the present invention provides a method for producing mixed fertilizer granules comprising a mixture of powdered dissolved phosphorous fertilizer and powdered silicic acid fertilizer and a binder, in which the powder mixture has a specific surface area of 500
~3000cm 2 /g, 10 to 60% by weight of particles with a particle size of 44 μm or less, and an appropriate amount of water to a blend of 100 parts by weight of the powder mixture and 1 to 7 parts by weight (calculated as MgSO 4 ) of magnesium sulfate-containing material as a binder. The present invention relates to a method for producing a mixed fertilizer granule, which is characterized by adding granules, granulating the mixture, and drying the mixture at 70 to 120°C. The powdered fertilized phosphorus fertilizer applied in the present invention is no different from that commonly used, and is made by mixing phosphate rock and magnesium silicate minerals such as serpentine rock, peridotite, or smelted nickel in a predetermined ratio. It is a glassy powder obtained by heating and melting a mixture, then rapidly cooling it with water, etc., and pulverizing it. In this case, trace elements such as boron, manganese, copper, zinc, or molybdenum may be present in the melted phosphorous fertilizer as necessary. In addition, the powdered siliceous fertilizer applied in the present invention is generally called silicic acid or magnetic silicic acid, and contains soluble silicic acid, alkali content, soluble magnesium, etc. Raw materials include slags, stainless steel slags, ferromanganese steel slags, silicomanganese slags, ferronitkel slags, nickel slags, ferrochrome slags, magnesium slags, and phosphorus production slags. The particle size and specific surface area of the mixture of powdered dissolved phosphorous fertilizer and powdered silicic acid fertilizer, together with the properties of the binder used, significantly affect the physical properties when granulated, so it is necessary to adjust them within a predetermined range. However, in the present invention, the above two powdered fertilizer mixtures have a specific surface area of 500 to 3000 cm 2 /g and a particle size of 500 to 3000 cm 2 /g.
It is most preferable to have a content of 10 to 60% of 44μ or less; outside this range, it tends to be difficult to satisfy the contradictory property requirements of water disintegration and granulation strength. Next, in the present invention, in granulating the above two powdered fertilizer mixtures, a substance containing magnesium sulfate is used as a binder, but this is not only industrial magnesium sulfate, but also the reaction between magnesium hydroxide and sulfuric acid. products, reaction products of magnesia and sulfuric acid, reaction products of serpentine or peridotite and sulfuric acid, etc. are mainly composed of MgSO 4 but also contain some MgCl 2 , Mg (OH) 2 may be included. Therefore, even if a certain amount of unreacted magnesium etc. is mixed in due to its nature, it can be used without any problem as long as it substantially contains magnesium sulfate. It may be of. The amount of magnesium sulfate-containing substances used in mixed fertilizers of powdered fused phosphorous fertilizer and powdered silicic acid fertilizer varies depending on manufacturing conditions and the physical properties of the mixture, but in most cases it is per 100 parts by weight of the powdered mixture. ,
1 to 7 parts by weight as MgSO4 , preferably 2 to 4 parts by weight
A range of parts by weight is appropriate. The reason for this is that if it is less than 1 part by weight, granulation becomes difficult, while if it is more than 7 parts by weight, it is not only uneconomical but also causes problems in terms of balance with the fertilizing ingredients. To granulate the above two powdered fertilizer mixtures using the magnesium sulfate-containing material, conventional granulation methods can be used without particular limitation, such as a dish granulator, a drum granulator, or a compression molding machine (press granulator). ), etc., to granulate it while adding an appropriate amount of water, then dry it at a temperature of 70 to 120°C until it becomes a substantially dehydrated product, and if necessary, classify it to produce a product. . In addition, unless the above drying conditions are met, not only will it be impossible to obtain granules having the following predetermined particle size with a good yield;
This is because the granules do not have enough strength to withstand storage and transportation. The size of granules is not uniform depending on the purpose, but
In most cases, a range of 0.5 to 5 mm, preferably 1 to 4 mm is appropriate, and those outside this range are returned to the initial step and reused. Thus, according to the production method of the present invention, a mixture of powdered dissolved phosphorous fertilizer and powdered silicate fertilizer, which has conventionally been difficult to form into granules, can be made into a desired mixture by adjusting the particle size and using a magnesium sulfate-containing substance. It can be granulated to a size of In addition, the obtained mixed fertilizer granules are endowed with soluble magnesium and sulfate roots, can be blended with other fertilizers and applied mechanically, and have good water disintegration and soil disintegration properties. It is something. In addition, it has appropriate strength, apparent specific gravity, and good texture with no dust generation, and is more compliant with the Offensive Odor Prevention Act, Water Pollution Prevention Act, Soil Pollution Prevention Act, Industrial Hygiene Act, etc. compared to granulated products that use organic materials as binders. The present invention has great industrial significance because it can be manufactured without causing any problems in compliance with the various laws and regulations, and can be handled safely in use. Hereinafter, the present invention will be specifically described with reference to Examples. Examples 1 to 10 A mixture of the powdered dissolved phosphorus fertilizer and powdered silicic acid fertilizer shown in Table 1 was added with a predetermined amount of magnesium sulfate-containing material, and a mixture was prepared using a dish-type granulator (diameter 1000 m/m, depth 80 m). /m, rotation speed 12r.pm, inclination angle 54°) and spray with water until the particle size is 1~4mm (preferably 2mm).
3 mm). Dry this (70
~120℃) Moisture content should be 0.1% or less. After cooling, this product was sized to a particle size of 1 to 4 m/m, and this ratio was taken as the yield rate to obtain a mixed fertilizer granule of powdered melted phosphorous fertilizer and powdered silicate fertilizer. Table 1 shows the test results for average crushing strength, water disintegration, and soil disintegration for this product.
Shown below.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 粉末溶成燐肥及び粉末珪酸質肥料の混合物と
結合剤よりなる混合肥料造粒物の製法において、
該粉末混合物を比表面積500〜3000cm2/g、粒度
44μm以下のもの10〜60重量%とし、その粉末混
合物100重量部と結合剤として硫酸マグネシウム
含有物1〜7重量部(MgSO4換算)との配合物
に適量の水を加えて造粒し、70〜120℃で乾燥す
ることを特徴とする混合肥料造粒物の製法。
1. In a method for producing mixed fertilizer granules comprising a mixture of powdered dissolved phosphorous fertilizer and powdered silicic acid fertilizer and a binder,
The powder mixture has a specific surface area of 500 to 3000 cm 2 /g and a particle size of
10 to 60 parts by weight of particles of 44 μm or less, and granulate by adding an appropriate amount of water to a blend of 100 parts by weight of the powder mixture and 1 to 7 parts by weight (calculated as MgSO4 ) containing magnesium sulfate as a binder, A method for producing mixed fertilizer granules characterized by drying at 70 to 120°C.
JP29884A 1984-01-06 1984-01-06 Granule of fused phosphate and silicious fertilizer mixture Granted JPS60145984A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29884A JPS60145984A (en) 1984-01-06 1984-01-06 Granule of fused phosphate and silicious fertilizer mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29884A JPS60145984A (en) 1984-01-06 1984-01-06 Granule of fused phosphate and silicious fertilizer mixture

Publications (2)

Publication Number Publication Date
JPS60145984A JPS60145984A (en) 1985-08-01
JPH0442357B2 true JPH0442357B2 (en) 1992-07-13

Family

ID=11469989

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29884A Granted JPS60145984A (en) 1984-01-06 1984-01-06 Granule of fused phosphate and silicious fertilizer mixture

Country Status (1)

Country Link
JP (1) JPS60145984A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2604633B2 (en) * 1989-08-11 1997-04-30 小野田化学工業株式会社 Porous siliceous granules

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52117772A (en) * 1976-03-24 1977-10-03 Dan Kakou Kk Additonal granulation of manuring effective minor component in single and compound synthetic fertilizers
JPS5520247A (en) * 1978-07-31 1980-02-13 Nippon Zeon Co Soil culture material
JPS5527840A (en) * 1978-08-16 1980-02-28 Hounou Hiriyou Kogyo Kabushiki Manufacture of fused phosphate

Also Published As

Publication number Publication date
JPS60145984A (en) 1985-08-01

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